JPH05262523A - Production of copper sulfate solution - Google Patents
Production of copper sulfate solutionInfo
- Publication number
- JPH05262523A JPH05262523A JP9006992A JP9006992A JPH05262523A JP H05262523 A JPH05262523 A JP H05262523A JP 9006992 A JP9006992 A JP 9006992A JP 9006992 A JP9006992 A JP 9006992A JP H05262523 A JPH05262523 A JP H05262523A
- Authority
- JP
- Japan
- Prior art keywords
- metallic
- powder
- suspension
- sulfuric acid
- stirrer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G3/00—Compounds of copper
- C01G3/10—Sulfates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は金属銅粉から硫酸銅溶液
を簡便に製造する方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for easily producing a copper sulfate solution from metallic copper powder.
【0002】[0002]
【従来の技術】金属銅粉から硫酸銅溶液を製造する一般
的な方法は、金属銅粉を焙焼して酸化銅粉とし、これを
硫酸に溶解するというものである。これは金属銅を直接
硫酸で溶解するには熱濃硫酸による酸化力を要し、この
溶解反応を大規模に行うには安全上設備に費用がかかり
過ぎるためである。2. Description of the Related Art A general method for producing a copper sulfate solution from metallic copper powder is to roast metallic copper powder into copper oxide powder, which is then dissolved in sulfuric acid. This is because the ability to oxidize metallic copper directly with sulfuric acid requires the oxidizing power of hot concentrated sulfuric acid, and the facility is too expensive for safety in carrying out this dissolution reaction on a large scale.
【0003】酸化銅粉の製造には例えばロータリーキル
ンなどが使用できるが、600℃程度の焙焼温度で金属
銅粉500kgを処理するのに5時間程かかり、得られ
た酸化銅粉を溶解する設備も別に必要であり、熱濃硫酸
溶解方式に比べてトータルコストは低いとは言え、燃料
代の節約、焙焼時間の短縮等課題は多い。A rotary kiln or the like can be used to produce the copper oxide powder, but it takes about 5 hours to process 500 kg of the metal copper powder at a roasting temperature of about 600 ° C., and a facility for melting the obtained copper oxide powder. Although the total cost is low compared to the hot concentrated sulfuric acid dissolution method, there are many problems such as saving fuel cost and shortening roasting time.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記事情に鑑
みて為されたものであり、酸化銅粉を経由することな
く、金属銅粉から直接硫酸銅溶液を安全に低コストで、
しかも短時間に製造し得る方法を提供するものである。The present invention has been made in view of the above circumstances, and it is possible to safely and inexpensively produce a copper sulfate solution directly from metallic copper powder without passing through copper oxide powder.
Moreover, it provides a method that can be manufactured in a short time.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
本発明の方法は、金属銅粉の懸濁液に微細な空気の泡を
多量に導入しながら該液を65乃至85℃に維持しつつ
硫酸を添加し、金属銅を酸化溶解する点に特徴がある。To achieve the above object, the method of the present invention is to maintain the liquid at 65 to 85 ° C. while introducing a large amount of fine air bubbles into a suspension of metallic copper powder. Meanwhile, it is characterized in that sulfuric acid is added to oxidize and dissolve metallic copper.
【0006】[0006]
【作用】金属銅粉の粒度は40乃至120メッシュが適
当である。粒度が小さい程溶解速度は速くなるが、あま
り粒度が小さいと取り扱い中に粉塵になり易く、作業環
境を悪化する上、懸濁液も作りにくい。The proper particle size of the metallic copper powder is 40 to 120 mesh. The smaller the particle size, the faster the dissolution rate, but if the particle size is too small, it will easily become dust during handling, which will worsen the working environment and make it difficult to form a suspension.
【0007】微細な空気の泡を多量に導入するには、撹
拌機の上部にある空気取入口から空気を自吸式に取入
れ、シャフトの中を通って翼の先端から排出する撹拌機
を備えた溶解槽が適当である。微細な空気泡が金属銅粉
の酸化に極めて効果的に働き、比較的短時間で酸化溶解
を完了する。In order to introduce a large amount of fine air bubbles, a stirrer is provided which takes in air from the air intake at the top of the stirrer in a self-priming manner and discharges it from the tip of the blade through the shaft. A dissolution tank is suitable. The fine air bubbles act extremely effectively on the oxidation of the copper metal powder, and complete the oxidative dissolution in a relatively short time.
【0008】空気排出口の直径は小さい程空気の泡は小
さくなり、酸化効率は良くなるが、あまり小さいと空気
中のゴミ等で閉塞する恐れもあるので、5乃至10mm
程度とするのが実際的である。The smaller the diameter of the air discharge port, the smaller the air bubbles and the better the oxidation efficiency, but if it is too small, it may be blocked by dust in the air, so it is 5 to 10 mm.
It is practical to set the degree.
【0009】又、撹拌翼の回転数は大きい程泡は微細に
なり溶解効率は上昇するが、金属銅から硫酸銅への転化
率が99%に達した後はそれ以上回転数を上げることは
無駄であり、最適の回転数を実験的に求めれば良い。実
験によると、100乃至125r.p.m.が適当な回
転数とも言える。Further, as the number of revolutions of the stirring blade increases, the bubbles become finer and the dissolution efficiency increases, but after the conversion rate from metallic copper to copper sulfate reaches 99%, the number of revolutions cannot be further increased. It is wasteful, and the optimum number of revolutions should be experimentally obtained. According to experiments, 100 to 125 r.p.m. p. m. Can be said to be an appropriate number of rotations.
【0010】前記転化率にとって液温も重要であり、高
い程有利である。しかしながら温度をあまり上げること
は液の蒸発による環境悪化、装置の腐食を招くので好ま
しくなく、65乃至85℃が適当な範囲である。The liquid temperature is important for the conversion rate, and the higher the temperature, the more advantageous. However, raising the temperature too much is not preferable because it causes environmental deterioration due to liquid evaporation and corrosion of the apparatus, and 65 to 85 ° C. is an appropriate range.
【0011】硫酸の添加は一度に行うよりも酸化反応に
従って添加するのがよく、所要量を1時間程度掛けて徐
々に添加すると良い。Sulfuric acid is preferably added according to the oxidation reaction rather than all at once, and it is advisable to add the required amount gradually over a period of about 1 hour.
【0012】このような方法で金属銅粉懸濁液を処理す
るとほぼ3時間で転化率99%以上で硫酸銅溶液を得る
ことができ、エネルギー的にも、時間的にも従来法より
有利である。When the metal copper powder suspension is treated by such a method, a copper sulfate solution with a conversion of 99% or more can be obtained in about 3 hours, which is more advantageous in energy and time than the conventional method. is there.
【0013】[0013]
実験No.1…1.5m3 容量のジャケット付槽と空気
自吸式撹拌機を有する溶解装置に工業用水920lを入
れ、粒度が40乃至60メッシュの金属銅粉125kg
を投入して懸濁させた後、撹拌機の回転数を125r.
p.m.とし、98%濃硫酸225kgを約1時間かけ
て添加した。この間液温を70℃に維持し、撹拌を更に
2時間続けた。硫酸銅への転化率は99.2%であっ
た。Experiment No. 1 ... 1.5 m 3 volume of jacketed tank and 920 l of industrial water was put into a dissolution apparatus having an air self-priming stirrer, and 125 kg of metal copper powder having a particle size of 40 to 60 mesh
Was added and suspended, and then the rotation speed of the stirrer was changed to 125 r.p.m.
p. m. And 225 kg of 98% concentrated sulfuric acid was added over about 1 hour. During this time, the liquid temperature was maintained at 70 ° C., and stirring was continued for another 2 hours. The conversion rate to copper sulfate was 99.2%.
【0014】実験No.2…実験No.1の溶解装置を
大型化した容量12m3 の装置に、砒素18g/l、銅
30g/l、硫酸90g/lを含有する溶液10m3 を
入れ、これに粒度が80乃至120メッシュの金属銅粉
500kgを投入して懸濁させ、撹拌速度を100r.
p.m.とし、98%濃硫酸287kgを約2時間で添
加し、この間液温を75乃至80℃の間に維持しながら
更に1時間撹拌を続けた。金属銅粉の硫酸銅への転化率
は99.0%であった。Experiment No. 2 ... Experiment No. Into a device with a capacity of 12 m 3 in which the dissolution device of 1 was enlarged, 10 m 3 of a solution containing 18 g / l of arsenic, 30 g / l of copper and 90 g / l of sulfuric acid was put, and a copper metal powder having a particle size of 80 to 120 mesh 500 kg was added to suspend and the stirring speed was 100 r.
p. m. Then, 287 kg of 98% concentrated sulfuric acid was added in about 2 hours, and stirring was continued for another hour while maintaining the liquid temperature at 75 to 80 ° C. The conversion rate of metal copper powder into copper sulfate was 99.0%.
【0015】[0015]
【発明の効果】本発明により金属銅粉から硫酸銅溶液を
直接、安全かつ低コストでしかも短時間で製造できるよ
うになった。According to the present invention, a copper sulfate solution can be directly produced from metallic copper powder, safely, at low cost and in a short time.
Claims (1)
に導入しながら該液を65乃至85℃に維持しつつ硫酸
を添加し、金属銅を酸化溶解することを特徴とする硫酸
銅溶液の製造方法。1. A method of introducing a large amount of fine air bubbles into a suspension of metal copper powder, adding sulfuric acid while maintaining the liquid at 65 to 85 ° C., and oxidizing and dissolving the metal copper. Method for producing copper sulfate solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9006992A JPH05262523A (en) | 1992-03-17 | 1992-03-17 | Production of copper sulfate solution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9006992A JPH05262523A (en) | 1992-03-17 | 1992-03-17 | Production of copper sulfate solution |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05262523A true JPH05262523A (en) | 1993-10-12 |
Family
ID=13988252
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9006992A Pending JPH05262523A (en) | 1992-03-17 | 1992-03-17 | Production of copper sulfate solution |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05262523A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004022486A1 (en) * | 2002-09-05 | 2004-03-18 | Nikko Materials Co., Ltd. | High purity copper sulfate and method for production thereof |
US7695527B2 (en) | 2003-09-04 | 2010-04-13 | Nippon Mining & Metals Co., Ltd | High purity copper sulfate and method for production thereof |
JP2011032126A (en) * | 2009-07-31 | 2011-02-17 | Jgc Catalysts & Chemicals Ltd | Method for producing aqueous copper sulfate solution |
JP2022109497A (en) * | 2021-01-15 | 2022-07-28 | 日本リサイクルセンター株式会社 | Method for producing aqueous solution of copper sulfate |
WO2024005307A1 (en) * | 2022-06-28 | 2024-01-04 | 고려아연 주식회사 | Method for preparing copper sulfate electrolytic solution |
-
1992
- 1992-03-17 JP JP9006992A patent/JPH05262523A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004022486A1 (en) * | 2002-09-05 | 2004-03-18 | Nikko Materials Co., Ltd. | High purity copper sulfate and method for production thereof |
CN1301910C (en) * | 2002-09-05 | 2007-02-28 | 日矿金属株式会社 | High purity copper sulfate and method for production thereof |
US7887603B2 (en) | 2002-09-05 | 2011-02-15 | Jx Nippon Mining & Metals Corporation | High purity copper sulfate and method for production thereof |
US8152864B2 (en) | 2002-09-05 | 2012-04-10 | Jx Nippon Mining & Metals Corporation | Method for production of high purity copper sulfate |
US7695527B2 (en) | 2003-09-04 | 2010-04-13 | Nippon Mining & Metals Co., Ltd | High purity copper sulfate and method for production thereof |
JP2011032126A (en) * | 2009-07-31 | 2011-02-17 | Jgc Catalysts & Chemicals Ltd | Method for producing aqueous copper sulfate solution |
JP2022109497A (en) * | 2021-01-15 | 2022-07-28 | 日本リサイクルセンター株式会社 | Method for producing aqueous solution of copper sulfate |
WO2024005307A1 (en) * | 2022-06-28 | 2024-01-04 | 고려아연 주식회사 | Method for preparing copper sulfate electrolytic solution |
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